US7781369B2 - Mesoporous silica thick-film, process for producing the same, adsorption apparatus and adsorbing film - Google Patents
Mesoporous silica thick-film, process for producing the same, adsorption apparatus and adsorbing film Download PDFInfo
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- US7781369B2 US7781369B2 US11/918,894 US91889406A US7781369B2 US 7781369 B2 US7781369 B2 US 7781369B2 US 91889406 A US91889406 A US 91889406A US 7781369 B2 US7781369 B2 US 7781369B2
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28078—Pore diameter
- B01J20/28083—Pore diameter being in the range 2-50 nm, i.e. mesopores
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D13/00—Electrophoretic coating characterised by the process
- C25D13/02—Electrophoretic coating characterised by the process with inorganic material
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D9/00—Electrolytic coating other than with metals
- C25D9/04—Electrolytic coating other than with metals with inorganic materials
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249953—Composite having voids in a component [e.g., porous, cellular, etc.]
- Y10T428/249967—Inorganic matrix in void-containing component
- Y10T428/249969—Of silicon-containing material [e.g., glass, etc.]
Definitions
- the present invention relates to a mesoporous silica thick-film, a process for producing the same, an adsorption apparatus, and an adsorbing film.
- Porous materials have been utilized in various fields such as adsorption and separation. According to IUPAC, porous materials are classified into microporous ones having a fine pore diameter of 2 nm or less, mesoporous ones having a fine pore diameter of 2 to 50 nm, and macroporous ones having a fine pore diameter of 50 nm or more.
- the microporous porous materials have conventionally been known and zeolites such as natural aluminosilicate salts and synthetic aluminosilicate salts, metal phosphate salts, and the like are known. They have been utilized for selective adsorption and form-selective catalytic reactions, and as molecular-size reaction vessels, in which the fine pore size of the fine pores is utilized.
- mesoporous silica having a homogeneous pores with narrow pore size distribution in nanometer level are regularly arranged. It has a structure where the pores having an equal diameter are arranged in a honeycomb form. In comparison with the conventional porous materials such as zeolite, it has characteristics that the fine pore volume is large and the surface area is also large. Silica gel has a disordered porous structure and silica gel having such a high specific surface area and such a large pore volume has not been known.
- silica is achieved through an action of a surfactant aggregate as a template.
- surfactant aggregate is not only very useful materials as catalysts for bulky molecules which do not enter the pores of zeolite, but also may be applied to functional materials such as optical materials and electronic materials by introducing guest species having various functions into the fine pores.
- the mesoporous silica is specifically known as a material called MCM-41 synthesized by hydrolyzing alkoxides of silicon in the presence of a surfactant as described in Non-Patent Document 1 and a material called FSM-16 synthesized by intercalating an alkylammonium between layers of kanemite, which is one type of layered silicic acid, as described in Non-Patent Document 2.
- Non-Patent Document 2 describes a production process wherein it is produced by ion-exchange of kanemite, which is one type of layered silicate salts with a surfactant.
- Non-Patent Document 4 describes a process for producing an inorganic porous body by forming a three-dimensional highly regular composite of inorganic material-surfactant as a precipitate through hydrothermal synthesis using an aggregate of a surfactant consisting of an alkyltrimethylammonium as a template, subjecting the composite to solid-liquid separation and washing, and then removing organic substances contained therein through calcination.
- the concentration of the surfactant is determined to be a concentration higher than the critical micelle concentration and lower than the liquid crystalline phase-forming concentration, e.g., 25 wt % and the pH of the solution is from 10 to 13.
- standard reaction temperature is 100° C.
- the porous body obtained by the hydrothermal synthesis has remarkably homogenous mesopore diameter as compared with the conventional porous materials and has a characteristic structure where the fine pores are regularly arranged.
- Patent Document 2 silica mesostructure thin film formed on a polymer compound film provided on a substrate wherein the thin film is formed on part or all of the polymer compound film having structural anisotropy imparted on the surface by linear polarized light irradiation
- Patent Document 3 a method of maintaining alkaline pH in an aqueous solution containing a surfactant and heating the whole to remove the surfactant
- Patent Document 4 A method by spin coating (Patent Document 4) and the like are known.
- the mesoporous silica of the porous material has a characteristic that it has a regular arrangement such as lamella, hexagonal, or cubic one or, even when it has no regular arrangement, has homogeneous mesopores. Since it has a large pore volume and a large number of hydroxyl groups are present on the surface of the fine pore wall, absorbed amount of water is large.
- a water absorbent has been developed and applications to an absorbent for separation, a sensor, a support for catalysts, and a fuel cell have been investigated, as well as studies for producing a film thereof have been performed.
- the film has an excellent gas adsorbing property and also has a function of separating various substances. Therefore, a variety of processes for producing such a porous body having a void structure have been proposed.
- the aforementioned mesoporous silica is expected as an adsorbent for water and organic vapors based on its uniform and regular fine pore structure.
- a water vapor adsorbent since it exhibits a large adsorption and desorption amount in a specific narrow relative humidity range depending on a pore diameter and the adsorption is attributable to capillary condensation, it has a large potential as a novel adsorbent (moisture adsorbent) which requires small energy for regeneration, requires low temperature for regeneration, and has a large adsorption amount.
- moisture adsorbent moisture adsorbent
- Such adsorption properties are excellent properties which are not exhibited by conventionally often employed zeolites and silica gel.
- an adsorbent is applied to an actual adsorption system (e.g., desiccant air conditioning), it is necessary to fix an adsorbent on a suitable substrate.
- a honeycomb rotor usually, a ceramic paper or the like is used.
- For supporting an adsorbent on the honeycomb rotor it is necessary to carry out steps of dispersing the adsorbent into a solution to form a slurry with a binder, impregnating a parent material of the honeycomb rotor therewith, and then drying and calcining the same.
- the adsorbent is used as an adsorbent for an adsorbtion heat pump, it is considered that it is desirable to fix the adsorbent on a metal fin from the viewpoint of improving heat-transfer properties.
- a known process for producing a mesoporous SiO 2 thin-film having a three-dimensional structure which includes obtaining an organo-inorgano composite SiO 2 thin-film having a three-dimensional structure formed on the base material by mixing an alkylene oxide block copolymer and a tetraalkyl orthosilicate in an ethanol solution, effecting hydrolysis with adjusting the solution to a low pH region to form a sol solution, dropping the sol solution onto a substrate, rotating the substrate at a high speed, and evaporating the solvent to effect gelation; and subsequently sintering the thin-film (Patent Document 6) and the like process.
- mesoporous silica is regularly deposited, i.e., homogeneous pore channels are directed to a transverse direction in this kind of mesoporous material
- a stress is to be applied from a lateral side of the fine pore channels, i.e., from above during a processing step.
- This kind of the mesoporous material having a honeycomb structure is weak in mechanical strength of the lateral side of the fine pore channels. Therefore, a conventional mesoporous film is apt to be broken at the fine pores during the above processing step.
- the mesoporous material where the homogeneous pore channels are directed to a transverse direction cannot virtually be utilized as a separating film. This is also true in the case where it is utilized as a chemical sensor.
- the mesoporous material as a high-density recording medium, it becomes possible to utilize it as a high-density recording medium only when individual fine pores act as recording units. Therefore, when the fine pore channels are directed to a transverse direction, reading and writing are difficult and effective surface area participating in recording is small, so that effects are difficult to be exhibited.
- the conventionally known mesoporous silica film is limited to a ⁇ m-order thin-film and no thick-film has been produced yet.
- the film thickness may be adjusted by a direct dip coating method or the like onto a substrate, actually, the film cannot be formed in an arranged state having a regular structure, so that it becomes difficult to form a thick-film.
- mesoporous silica is expected to be as an adsorbent for water and organic vapors owing to its homogeneous and ordered mesopore structure.
- mesoporous silica since it is considered as a water vapor adsorbent, since it exhibits a large adsorption and desorption amount in a specific narrow relative humidity range depending on a mesopore diameter and the adsorption is attributable to capillary condensation, it has a large potential as a novel adsorbent (moisture absorbent) which requires small energy for regeneration, requires low temperature for regeneration, and has a large adsorption amount. Owing to the adsorbing properties, it becomes possible to obtain a film which allows development of an air-cleaning system having excellent properties which are not exhibited by conventionally often employed zeolites and silica gel.
- Patent Document 1 WO91/11390
- Patent Document 2 JP-A-2002-338229
- Patent Document 3 JP-A-2004-27270
- Patent Document 4 JP-A-2002-250713
- Patent Document 5 Japanese Patent Application No. 2003-385662
- Patent Document 6 JP-A-2002-250713
- Patent Document 7 JP-A-2003-335516
- Patent Document 8 JP-A-2004-345895
- Non-Patent Document 1 Nature. Vol. 359, p. 710
- Non-Patent Document 2 Journal of Chemical Society Communications. Vol. 1993, p. 680
- Non-Patent Document 3 J. Am. Chem. Soc. 11410834 (1992)
- Non-Patent Document 4 Chemical Communications. Vol. 1996, p. 1149
- Non-Patent Document 5 Nature. Vol. 389, p. 364
- Non-Patent Document 6 Nature. Vol. 379, p. 703
- An object of the invention is to provide a thick-film mesoporous silica and a process for producing a thick-film mesoporous silica.
- the mesoporous silica powder is dispersed in a solvent.
- the mesoporous silica is necessarily dispersed homogenously and is desirably in the form of a fine powder (particle diameter: 40 ⁇ m or less).
- Electrode plates are placed in the dispersion of the mesoporous silica in the solvent and voltage in a range of from a finite value of 0 V or more to 1000 V is applied.
- the mesoporous silica is charged positive or negative, is migrated toward the anode electrode, and can be precipitated in an arranged state having a regular structure on the electrode surface.
- An amount of electrophoretic deposition increases depending on the passage of time within a specific period of time.
- the amount of electrophoretic deposition becomes constant.
- the relation between the amount of electrophoretic deposition per unit and electrophoretic deposition time also progresses similarly.
- the electrophoretic deposition time and the electrophoretic deposition thick-film also progress similarly.
- an electrophoretic deposited film having a desired thickness up to about 1 mm can be produced by controlling the voltage and the electrophoretic deposition time.
- a thick-film can be formed on a surface of the electrode plate in a state that a mesoporous silica is arranged as a regular structure by subjecting the mesoporous silica to electrophoretic deposition. Furthermore, it has been found that a 1 mm-order thick-film can be finally formed and fixed when the thick-film is treated at a temperature of 150 to 500° C.
- a mesoporous silica thick-film comprising a layer of mesoporous silica formed in a thickness of 10 ⁇ m to 1 mm.
- a process for producing a mesoporous silica thick-film which comprises disposing a substrate in a solution containing mesoporous silica suspended therein and subsequently applying a voltage thereby to form a film having a thickness of 10 ⁇ m to 1 mm by the electrophoretic deposition of the mesoporous silica on a surface of the substrate.
- the adsorption and desorption properties of the mesoporous silica thick-film for vapors and gases are superior to those of mesoporous silica powder itself, so that development of a novel adsorption and desorption apparatus becomes possible and also development of novel cleaning system and concentration system employing the same becomes possible.
- seed crystals can be applied rapidly and homogeneously as compared with the conventional slurry-infiltrating method.
- a film thickness to be formed can be precisely controlled by controlling the voltage and the deposition time.
- FIG. 1 is a figure showing a structure of mesoporous silica.
- FIG. 2 is a figure showing a electrophoretic deposition apparatus.
- FIG. 3 is a figure showing a relation between electrophoretic deposition time and the amount of electrophoretic deposition in the electrophoretic deposition of mesoporous silica from a mesoporous silica/acetone-based electrophoretic deposition bath.
- FIG. 4 is a figure showing an electrophoretic deposition.
- FIG. 5 is a figure showing a relation between electrophoretic deposition time and the amount of electrophoretic deposition per unit area.
- FIG. 6 shows a relation between electrophoretic deposition time and electrophoretic deposited film thickness.
- FIG. 7 is a figure showing a surface microscopic photograph of electrophoretic deposited film.
- FIG. 8 is a surface 3D image of electrophoretic deposited film.
- FIG. 9 is a figure showing a result of height distribution measurement of electrophoretic deposited film.
- FIG. 10 is a figure showing a result of nitrogen adsorption evaluation.
- FIG. 11 is a figure showing an X-ray diffraction pattern of mesoporous silica powder.
- FIG. 12 is a figure showing a mesoporous silica electrophoretic deposited film prepared on a stainless wire ( ⁇ 0.8 mm).
- FIG. 13 is a figure showing a mesoporous silica electrophoretic deposited film thinly prepared on an aluminum plate (5 mm ⁇ 50 mm).
- the mesoporous silica thick-film of the invention is a film formed of mesoporous silica in a thickness of 10 ⁇ m to 1 mm.
- the mesoporous silica may be any one having a hexagonal structure shown in FIG. 1 , a cubic structure, or the like so long as it has a homogeneous mesopore diameter in a range of 1 to 10 nm.
- the mesoporous silica thick-film is composed by arranging the mesoporous silica as a regular structure by electrophoretic deposition.
- the mesoporous silica thick-film is a mesoporous silica thick-film formed on a surface of a substrate.
- the substrate is formed of a conductive substance and is suitably adopted so long as it can be used as an electrode.
- the substrate include metal materials such as stainless steel, ordinary steel, low alloy steel, Al, and Cu, and non-metallic materials such as ceramics, glass, and pottery and porcelain.
- conductivity can be imparted by electroless plating of Ni, Cu, or the like or by coating a conductive ceramic such as ITO prior to the electrophoretic deposition.
- the substrate may be a plate shape or any other distorted shape such as tubular or prismatic one. Since a thick-film is formed on the substrate surface, in the case of using it with installation into an apparatus, a member constituting the apparatus can be used as the substrate. In the case that the substrate is distorted one such as tubular or prismatic one, the thick-film can be formed along the shape.
- the mesoporous silica for use in the formation of the thick-film of the invention has a homogeneous fine pore diameter in a range of 1 to 10 nm and may be any one such as those having the shape shown in FIG. 1 , a cubic structure or the like.
- the mesoporous silica for example, it can be synthesized by the spray-drying method shown below.
- a fine powdery mesoporous silica having a diameter of 10 ⁇ m or less can be synthesized.
- the mesoporous silica is desirably in a fine powdery shape (particle diameter: 40 ⁇ m or less). Therefore, according to the spray-drying method, a homogeneously dispersed mesoporous silica suspension can be obtained.
- mesoporous silica having a particle diameter of 40 ⁇ m or less which is obtained by pulverizing or classifying mesoporous silica synthesized by hydrothermal synthesis or solvent evaporation.
- the spray-drying method is as follows.
- a silicate compound is added thereto and the whole is stirred in the presence of an acid and a surfactant to achieve hydrolysis.
- an alkyl silicate, an alkoxy silicate, or the like can be employed.
- the acid is not limited to a particular acid. Owing to easy handling and availability, an aqueous hydrochloric acid solution can be added and used.
- a surfactant a cationic or nonionic surfactant can be used.
- the treating temperature may be an ordinary temperature.
- a hydrolyzate solution of the silicate compound can be obtained.
- the solution is sprayed by means of a spray dryer to evaporate the solvent, thereby obtaining a white powder.
- the resulting white powder is calcined to remove the template (the cationic or nonionic surfactant).
- the calcination temperature is suitably determined. In general, it is 500 to 700° C.
- a mesoporous silica having a three-dimensional regularity having a homogeneous fine pore diameter ranging from 1 to 10 nm can be obtained.
- FIG. 2 is a figure showing an apparatus for the electrophoretic deposition for use in the invention.
- a solvent is charged into the apparatus for the electrophoretic deposition in the vessel of a messcylinder 4 and the mesoporous silica obtained in the above step of producing the mesoporous silica is dipersed therein.
- the solvent water or an organic solvent may be suitably used.
- an alcohol a ketone such as acetone, hexane, or the like can be used.
- the charging behavior of the mesoporous silica powder in a solvent varies depending on the kind of the solvent and the process for producing the mesoporous silica powder and the powder may be charged positive or negative.
- the substrate is used as an anode and a stainless net is used as a counter electrode. These electrodes are disposed. A known electrode can be used accordingly.
- the mesoporous silica powder can be electrophoresis on the surface of a tubular stainless substrate 1 .
- a fine thick-film of the mesoporous silica can be formed.
- the voltage varies depending on the ability of the apparatus for the electrophoretic deposition. As the voltage by means of a direct current voltmeter 5 , a value in the range of from a finite value of 0 V or more to 1000 V is adopted.
- range of from a finite value of 0 V or more to 1000 V means that it is essential to apply voltage in the electrophoretic deposition in the invention. Specifically, since the electrophoretic deposition cannot be achieved when the value of the voltage on that occasion is 0 V, it means that the range does not include voltage 0 and the voltage may be a value exceeding 0 V, for example, 0.01, 0.1, 1, or 100 V. In conclusion, it means that the invention is practicable when the voltage having a value exceeding 0 V and up to 1000 V is applied.
- the amount of electrophoretic deposition increases depending on the passage of time within a specific period of time. When the specific period of time is passed, the increase in the amount of electrophoretic deposition disappears, and the amount of electrophoretic deposition takes a constant value ( FIG. 3 ).
- the relation between the amount of electrophoretic deposition per unit and the electrophoretic deposition time progresses similarly ( FIG. 5 ). Moreover, the electrophoretic deposition time and the electrophoretic deposited thick-film also progress similarly ( FIG. 6 ).
- the mesoporous silica thick-film formed on the substrate, which is obtained in the above step, is taken out and the solvent attached is removed by treating it at 150 to 500° C., whereby a mesoporous silica thick-film composed of a dense film can be formed.
- the structure is shown in FIG. 7 , FIG. 8 , and FIG. 9 .
- mesoporous silica thick-film By subjecting the resulting mesoporous silica thick-film to X-ray diffraction analysis (XRD) of mesoporous silica, it can be confirmed that the mesoporous silica in the thick-film has a high three-dimensional regularity.
- XRD X-ray diffraction analysis
- the mesoporous silica thick-film by subjecting the mesoporous silica thick-film to a test whether it has a gas adsorbing ability or not, the gas adsorbing ability can be investigated.
- the fine pore structure of the resulting mesoporous silica thick-film is evaluated using a nitrogen-adsorption measuring apparatus (Belsorp-mini, manufactured by Bel Japan, Inc.). The results are as shown in FIG. 10 .
- the nitrogen-adsorption isotherms of the mesoporous silica powder, a mesoporous silica thick-film formed on a stainless substrate by electrophoretic deposition (EPD), and a mesoporous silica thick-film after heat treatment at 300° C. all exhibit IV-type isothermal curves (according to the classification of IUPAC) characteristic to porous materials having mesopores, and it is found that an original highly regular fine pore structure is maintained even after EPD and heat treatment.
- the mesoporous silica obtained in the invention is found to have an adsorbing ability of steam and organic vapors owing to the homogeneous and regular fine pore structure.
- it since it is considered as a water vapor adsorbent, since it exhibits a large adsorption and desorption amount in a specific narrow relative humidity range depending on the homogeneous pore diameter and the adsorption is attributable to capillary condensation, it has a large potential as a novel adsorbent (moisture absorbent) which requires a small energy for regeneration, is capable of regeneration at low temperature, and has a large adsorption amount.
- moisture absorbent moisture absorbent
- the mesoporous silica in an air-cleaning system having excellent properties which are not exhibited by conventionally employed zeolites and silica gel, as well as air-cleaning facilities for various production lines. Furthermore, it is possible to utilize it in an apparatus for concentrating a dilute gas by adsorption treatment.
- the hydrolyzate solution was transferred into a 500 ml of an round-bottom flask and was reacted at a temperature of 25° C. in a reduced pressure state of 70 hPa for 1 hour and 24 minutes using a rotary evaporator (38 rpm).
- the resulting white powder was calcined at 600° C. to remove the cationic or nonionic surfactant.
- XRD X-ray diffraction analysis
- the mesoporous silica powder obtained by the above synthetic process was added to water or an organic solvent in a ratio of 0.1 g per 30 ml of the medium and the whole was irradiated with ultrasonic wave for 10 minutes, thereby a electrophoretic deposition bath being obtained.
- the particle size of the mesoporous silica used in the preliminary experiment was 10 ⁇ m or less in the electrophoretic deposition bath. However, a particle size of 40 ⁇ m or less may be sufficient.
- the organic solvent an alcohol such as methanol, ethanol, or 1-propanol, a ketone such as acetone, and hexane was used.
- the apparatus for electrophoretic deposition is shown in FIG. 2 .
- the mesoporous silica powder is electrophoresis and the mesoporous silica powder was applied on the surface of the tubular stainless substrate.
- a good thick-film of the mesoporous silica could be formed.
- the amount of electrophoretic deposition per unit area of the substrate reached about 24 mg/cm 2 within 10 minutes of electrophoretic deposition time ( FIG. 5 ) and a thick-film having a film thickness of up to about 240 ⁇ m could be formed ( FIG. 6 ).
- the amount of electrophoretic deposition increases depending on the passage of time within a certain specific period of time. When the time zone is passed, the amount of electrophoretic deposition becomes constant.
- the relation between the amount of electrophoretic deposition per unit and electrophoretic deposition time also progresses similarly.
- the electrophoretic deposition time and the electrophoretic deposited thick-film also progress similarly.
- the electrophoretic mobility was found to be about ⁇ 2.4 ⁇ 10 ⁇ 6 cm 2 /Vs and zeta-potential was found to be about ⁇ 40 V, so that it was supported that the mesoporous silica was charged negative and was electrically migrated toward the anode when voltage was applied.
- FIG. 4 The surface and the cross-sectional structure of a sample ( FIG. 4 ) which had been obtained by electrophoretic deposition at 50 V for 10 minutes with adding 1.4 g of the mesoporous silica to 140 ml of acetone using a tubular stainless tube having a surface area (right face) of 15.7 cm 2 as an anode substrate using an experimental apparatus shown in FIG. 2 were observed on a confocal microscope.
- a broken surface where the electrodeposited mesoporous silica film had been partially peeled off was observed from above, the surface of the electrophoretic deposition was smooth ( FIG. 7 ).
- FIG. 8 when the broken surface was observed from an oblique direction, a mesoporous silica-deposited layer having a homogeneous thickness was formed ( FIG. 8 ). Also from height distribution measurement at a line A to B in FIG. 7 , it was found that the electrophoretic deposition was deposited smoothly in a thickness of about 240 ⁇ m onto the substrate ( FIG. 9 ).
- the fine pore structure of the resulting film was evaluated using a nitrogen-adsorption measuring apparatus (Belsorp-mini, manufactured by Bel Japan, Inc.). The results are shown in FIG. 10 .
- the nitrogen-adsorption isothermal curves of the mesoporous silica powder, the mesoporous silica thick-film formed on a stainless substrate by EPD, and the mesoporous silica thick-film after heat treatment at 300° C. all exhibited IV-type isothermal curves (according to the classification of IUPAC) characteristic to porous bodies having mesopores and it was found that an original highly regular fine pore structure was maintained even after EPD and heat treatment.
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Abstract
Description
-
- 1 tubular stainless substrate
- 2 electrophoretic deposition bath
- 3 counter electrode
- 4 messcylinder
- 5 direct current voltmeter
TABLE 1 |
Electrophoretic deposition conditions and polarity and amount of electrophoretic deposition |
Amount of | ||||||||||
Amount | Weight before | Weight after | Amount of | Electrophoretic | ||||||
of | Kind of | Amount of | electrophoretic | electrophoretic | Electrophoretic | deposition per unit | ||||
Solvent | solvent | powder | powder | Voltage | Time | Polarity | deposition (g) | deposition (g) | deposition (g) | area g/cm2 |
MeOH | 30 ml | Calcined | 0.105 | g | 50 | V | 3 | min | + | 0.34029 | 0.34029 | 0 | 0.000000 |
powder | − | 0.35316 | 0.35326 | 0.0001 | 0.000006 | ||||||||
EtOH | 30 ml | Calcined | 0.0981 | g | 50 | V | 3 | min | + | 0.35077 | 0.35077 | 0 | 0.000000 |
powder | − | 0.33802 | 0.33807 | 5E−05 | 0.000003 | ||||||||
1-PrOH | 30 ml | Calcined | 0.0989 | g | 50 | V | 3 | min | + | 0.34912 | 0.34937 | 0.00025 | 0.000016 |
powder | − | 0.34343 | 0.34361 | 0.00018 | 0.000011 | ||||||||
2-PrOH | 30 ml | Calcined | 0.1056 | g | 50 | V | 3 | min | + | 0.33008 | 0.33016 | 8E−05 | 0.000005 |
powder | − | 0.34852 | 0.34867 | 0.00015 | 0.000010 | ||||||||
Acetone | 30 ml | Calcined | 0.0973 | g | 50 | V | 3 | min | + | 0.33294 | 0.35245 | 0.01951 | 0.001243 |
powder | − | 0.33954 | 0.34038 | 0.00084 | 0.000054 | ||||||||
Acetone | 30 ml | uncalcined | 0.1002 | g | 50 | V | 3 | min | + | 0.33184 | 0.33357 | 0.00173 | 0.000110 |
powder | − | 0.35023 | 0.35031 | 8E−05 | 0.000005 | ||||||||
Acetone | 30 ml | spray-dried | 0.1048 | g | 50 | V | 3 | min | + | 0.33126 | 0.33563 | 0.00437 | 0.000278 |
powder | − | 0.33551 | 0.3371 | 0.00159 | 0.000101 | ||||||||
Hexane | 30 ml | calcined | 0.1003 | g | 50 | V | 3 | min | + | 0.33591 | 0.33603 | 0.00012 | 0.000008 |
powder | − | 0.35020 | 0.35051 | 0.00031 | 0.00002 | ||||||||
H2O | 30 ml | calcined | 0.0996 | g | 2.5 | V | 10 | min | + | 0.35021 | 0.35031 | 0.00010 | 0.000006 |
powder | − | 0.33588 | 0.33595 | 0.00007 | 0.000004 | ||||||||
(3) Charging Properties of Mesoporous Silica Powder
Claims (20)
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JP5011026B2 (en) * | 2007-08-21 | 2012-08-29 | シャープ株式会社 | SPECIFIC GAS COMPONENT CONCENTRATION DEVICE USING POROUS STRUCTURE AND SPECIFIC GAS COMPONENT DETECTION DEVICE |
JP5190925B2 (en) * | 2007-10-31 | 2013-04-24 | 独立行政法人産業技術総合研究所 | Method for producing mesoporous silica thick film |
FR2929264B1 (en) * | 2008-03-31 | 2010-03-19 | Inst Francais Du Petrole | INORGANIC MATERIAL FORM OF SPHERICAL PARTICLES OF SPECIFIC SIZE AND HAVING METALLIC NANOPARTICLES TRAPPED IN A MESOSTRUCTURED MATRIX |
JP2010280121A (en) * | 2009-06-04 | 2010-12-16 | Tokyo Univ Of Science | Laminate of ceramic-based insulating layer and metal layer, and method for manufacturing the same |
JP5696283B2 (en) * | 2010-07-28 | 2015-04-08 | 株式会社船井電機新応用技術研究所 | Method for producing enzyme electrode |
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WO2006112505A1 (en) | 2006-10-26 |
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US20090082201A1 (en) | 2009-03-26 |
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